JPH06154762A - Method and device for separating ultrafine particles in muddy water treatment plant for excavating ground - Google Patents

Method and device for separating ultrafine particles in muddy water treatment plant for excavating ground

Info

Publication number
JPH06154762A
JPH06154762A JP30567692A JP30567692A JPH06154762A JP H06154762 A JPH06154762 A JP H06154762A JP 30567692 A JP30567692 A JP 30567692A JP 30567692 A JP30567692 A JP 30567692A JP H06154762 A JPH06154762 A JP H06154762A
Authority
JP
Japan
Prior art keywords
muddy water
electrode
water
ultrafine particles
water tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP30567692A
Other languages
Japanese (ja)
Other versions
JP2943539B2 (en
Inventor
Takeshi Kawachi
武 川地
Mitsuteru Sumida
光輝 炭田
Hirobumi Saito
博文 斉藤
Masaaki Yoshizaki
正明 吉崎
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Obayashi Corp
Original Assignee
Obayashi Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Obayashi Corp filed Critical Obayashi Corp
Priority to JP30567692A priority Critical patent/JP2943539B2/en
Publication of JPH06154762A publication Critical patent/JPH06154762A/en
Application granted granted Critical
Publication of JP2943539B2 publication Critical patent/JP2943539B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To provide a separating device incorporated in a muddy water treatment plant at a working site of a continuous underground wall or the like and carry out consistently, continuously and simply the separation of ultrafine particles in the muddy water out of the muddly water in an efficient manner by the electrophoresis phenomenon and remove aggregates of ulfrafine particles off electrodes. CONSTITUTION:A plurality of electrode panel elements 4 are disposed in a water tank 1 filled with muddy water, and direct current voltage is applied between electrode panel elements 4 facing each other in the muddy water to aggregate ultrafine particles in the muddy water on the surfaces of elements as positive electrodes by the electrophoresis phenomenon. The application polarity of direct current voltage is turned over as the aggregates stuck to the elements grow larger, and the elements to which the aggregates are adhering are converted from the positive to negative electrode to drop the aggregates off the surfaces of the elements and precipitate them down on the bottom of the water tank 1.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、連続地中壁工法、場
所打ち杭工法、泥水シールド工法などのように泥水を安
定液として用いて地盤を掘削する工法において、工事中
に発生する泥水を処理するプラントに関し、特に、一次
処理後の泥水中にコロイド状に含まれている超微粒子を
分離する方法および装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of excavating the ground by using mud as a stable liquid such as a continuous underground wall method, a cast-in-place pile method, and a mud shield method. More particularly, the present invention relates to a method and a device for separating ultrafine particles contained in colloidal form in mud water after primary treatment.

【0002】[0002]

【従来の技術】地盤を掘削する方法として、掘削孔壁の
安定性を保つために、掘削孔内に泥水を満たした状態で
掘削を進める泥水工法が知られている。この種の工法で
は、工事現場に付設したプラントで泥水を処理しながら
循環使用している。このプラントの処理対象は、循環泥
水とともに排出される掘削土砂の分離処理、余剰泥水お
よび劣化した廃棄泥水の処理などである。
2. Description of the Related Art As a method for excavating the ground, there is known a mud construction method for advancing the excavation while the excavation hole is filled with mud in order to maintain the stability of the excavation hole wall. In this type of construction method, muddy water is treated and circulated in a plant attached to the construction site. The treatment targets of this plant are separation of excavated soil discharged along with circulating mud, treatment of surplus mud and deteriorated waste mud.

【0003】泥水性状は、掘削土質、安定液材料(ベン
トナイト、CMC、ポリマー剤、分散剤など)の種類や
添加量によって変動する。処理の対象はコロイド粒子か
ら礫まで広範囲であり、一般に処理工程は3段階に分れ
ている。一次処理では、自然沈澱、強制沈澱、遠心分離
などの方法で泥水中の粗大固形分を分離除去する。一般
に一次処理では粒径74μm以上の礫、砂、および粘土
・シルト塊を分離する。二次処理では、一次処理された
分離水から粒径74μm以下の粘土・シルトなどを分離
除去する。三次処理では二次処理された分離水のPH調
整を行い、処理水を放流したり、あるいは工事用水とし
て再使用する。
The state of mud water varies depending on the type and amount of excavated soil, type of stabilizing liquid material (bentonite, CMC, polymer agent, dispersant, etc.). The target of treatment is a wide range from colloidal particles to gravel, and generally the treatment process is divided into three stages. In the primary treatment, coarse solids in mud water are separated and removed by a method such as natural precipitation, forced precipitation and centrifugation. Generally, the primary treatment separates gravel, sand, and clay / silt lumps having a particle size of 74 μm or more. In the secondary treatment, clay / silt having a particle size of 74 μm or less is separated and removed from the separated water subjected to the primary treatment. In the tertiary treatment, the pH of the secondary treated water is adjusted and the treated water is discharged or reused as construction water.

【0004】従来の代表的な二次処理では、泥水に凝集
剤を添加混合し、凝集されたフロックを強制脱水する方
法がとられている。脱水装置としては各種のものが開発
されており、一般にはフィルタープレス,ロールプレス
などの加圧式脱水機が多用されている。しかし、この種
の従来方法では泥水中にコロイド状に分散されている粘
土成分の超微粒子を充分に分離することができないとい
う問題があった。この問題を解決する手段として、本出
願人らは先に、特開平4−254690号に示すような
超微粒子の分離方法を開発した。
In a typical conventional secondary treatment, a method is used in which a flocculant is added to and mixed with mud water, and flocculated flocs are forcedly dehydrated. Various types of dewatering devices have been developed, and pressure dewatering machines such as filter presses and roll presses are commonly used. However, this type of conventional method has a problem that it is not possible to sufficiently separate the ultrafine particles of the clay component dispersed in colloidal form in the muddy water. As a means for solving this problem, the present applicants have previously developed a method for separating ultrafine particles as disclosed in JP-A-4-254690.

【0005】この方法では、一次処理後の泥水が入った
水槽内に2つの電極板を対向配置し、両電極に直流電圧
を印加し、泥水中の超微粒子を電気泳動現象により正電
極側に凝集させるのである。これにより泥水中の超微粒
子が分離されて澄んだ水が得られる。
In this method, two electrode plates are placed opposite to each other in a water tank containing mud water after the primary treatment, a DC voltage is applied to both electrodes, and ultrafine particles in the mud water are electrophoresed to the positive electrode side. To agglomerate. As a result, ultrafine particles in the muddy water are separated and clear water is obtained.

【0006】[0006]

【発明が解決しようとする課題】前述した電気泳動現象
を応用した泥水の処理方法について、実験室レベルでは
その有効性をはっきりと確認できたのであるが、実際の
工事現場にて要求される速度で能率よく超微粒子を分離
するには不充分であった。特に、電極に付着した超微粒
子の凝集塊を電極から簡単に取り除く手段が開発されて
いなかったため、次々に発生する大量の泥水を能率よく
処理することができなかった。
The effectiveness of the above-mentioned method for treating mud water applying the electrophoretic phenomenon was clearly confirmed at the laboratory level, but the speed required at the actual construction site was confirmed. However, it was not sufficient to efficiently separate ultrafine particles. In particular, since a means for easily removing the aggregate of ultrafine particles adhering to the electrode from the electrode has not been developed, it has been impossible to efficiently process a large amount of muddy water that is generated one after another.

【0007】この発明は前述した従来の問題点に鑑みな
されたもので、その目的は、連続地中壁などの工事現場
の泥水処理プラントに組み込まれ、電気泳動現象により
泥水中の超微粒子を能率よく分離することと、電極に付
着した超微粒子の凝集塊を電極から取り除くこととを一
貫して簡単に行えるようにすることにある。
The present invention has been made in view of the above-mentioned conventional problems, and an object thereof is to be incorporated in a muddy water treatment plant at a construction site such as a continuous underground wall to efficiently remove ultrafine particles in muddy water by an electrophoretic phenomenon. It is to make it possible to consistently and easily separate well and to remove the agglomerates of ultrafine particles adhering to the electrode from the electrode.

【0008】[0008]

【課題を解決するための手段】そこでこの発明では、泥
水が入った水槽内に複数の電極パネルエレメントを配設
し、泥水中で対向する前記電極パネルエレメント間に直
流電圧を印加し、泥水中の超微粒子を電気泳動現象によ
り正電極となっている前記エレメントの表面に凝集さ
せ、前記エレメントに付着した凝集塊が大きく成長した
後に前記直流電圧の印加極性を反転し、前記凝集塊が付
着した前記エレメントを正電極から負電極に変えること
で、前記凝集塊を前記エレメント表面から脱落させて前
記水槽底に沈澱させるようにした。
In the present invention, therefore, a plurality of electrode panel elements are arranged in a water tank containing muddy water, and a DC voltage is applied between the electrode panel elements facing each other in muddy water. Of the ultrafine particles are aggregated on the surface of the element, which is a positive electrode by an electrophoretic phenomenon, and the applied polarity of the DC voltage is reversed after the agglomerates adhered to the element grow large, and the agglomerates adhered. By changing the element from a positive electrode to a negative electrode, the agglomerate was dropped from the surface of the element and settled on the bottom of the water tank.

【0009】また、前記の方法を実施する超微粒子の分
離装置を、処理対象泥水が供給される水槽と、この水槽
内に配設された複数の電極パネルエレメントと、隣り合
って対向する前記電極パネルエレメント間に直流電圧を
印加するための直流電源と、この直流電源から前記電極
パネルエレメント間に印加する直流電圧の極性を切り換
えるための切り換え手段と、前記水槽の底部の沈澱物を
当該水槽外に排出する手段とで構成した。
Further, the ultrafine particle separating apparatus for carrying out the above method is provided with a water tank to which mud water to be treated is supplied, a plurality of electrode panel elements arranged in the water tank, and the electrodes facing each other. A direct current power source for applying a direct current voltage between the panel elements, a switching means for switching the polarity of the direct current voltage applied from the direct current power source between the electrode panel elements, and a precipitate at the bottom of the water tank outside the water tank. And means for discharging to.

【0010】[0010]

【作用】電気泳動現象により正電極エレメント側に泥水
中の超微粒子が引き寄せられて凝集するという分離の原
理は前記の従来技術と同じである。正電極エレメントに
相当量の超微粒子が凝集塊となって付着すると、泥水中
の超微粒子をさらに引き付けて凝集させる効果が大幅に
低下する。そこで前記電極パネルエレメントに印加して
いる直流電圧の極性を反転させると、電界の方向が逆に
なるため、正電極から負電極に切り替わったエレメント
に付着していた前記凝集塊が塊状態のままで脱落し、泥
水に分散することなく水槽底に沈澱する。したがって前
工程で超微粒子が分離されて澄んだ水は再び濁ることは
ない。塊になって底に沈澱した凝集塊を水槽外に排出す
るのは前記一次処理装置と同様な構成で簡単に行うこと
ができる。
The principle of separation is that the ultrafine particles in the muddy water are attracted to the positive electrode element side by the electrophoretic phenomenon and aggregated, which is the same as the above-mentioned prior art. When a considerable amount of ultrafine particles adhere to the positive electrode element as an aggregate, the effect of further attracting and aggregating the ultrafine particles in the muddy water is significantly reduced. Therefore, when the polarity of the DC voltage applied to the electrode panel element is reversed, the direction of the electric field is reversed, so that the agglomerate attached to the element switched from the positive electrode to the negative electrode remains in a clumped state. It will fall off and will settle on the bottom of the tank without being dispersed in muddy water. Therefore, the ultrafine particles are separated in the previous step and clear water does not become cloudy again. It is possible to easily discharge the agglomerated lumps that have formed into lumps and settled to the bottom to the outside of the water tank with the same configuration as that of the primary treatment device.

【0011】また、泥水中で対向する電極パネルエレメ
ントに直流電圧を印加すると、電気分解反応が起き、負
電極側から水素ガスが発生するが、このガス発生は前記
エレメントに付着していた凝集塊を電極表面から浮き上
がらせる剥離効果を生みだし、きわめて良好に凝集塊を
エレメントから脱落させることができる。
When a DC voltage is applied to the opposing electrode panel element in the muddy water, an electrolysis reaction occurs and hydrogen gas is generated from the negative electrode side. This gas generation is caused by the agglomerates attached to the element. It produces a peeling effect that causes the particles to float up from the electrode surface, so that the agglomerates can be dropped from the element very well.

【0012】[0012]

【実施例】図1〜図4はこの発明の一実施例による分離
装置の構成を示している。1は上面が開口した角形平面
の泥水槽であり、その長手方向に一端側に泥水を槽内に
供給するための入口2が設けられているとともに、他端
側には処理後の水を排出するための出口3が設けられて
いる。この泥水槽1内に、以下に説明する支持機構によ
って14枚の電極パネルエレメント4が配置される。電
極パネルエレメント4は槽内に垂直に挿入され、かつ泥
水槽1の長手方向に対して直交し、一定間隔をおいてほ
ぼ並行に並べられている。
1 to 4 show the construction of a separating apparatus according to an embodiment of the present invention. Reference numeral 1 is a rectangular flat mud tank with an open top surface, and an inlet 2 for supplying mud water into the tank is provided at one end side in the longitudinal direction, and the treated water is discharged at the other end side. An exit 3 is provided for In the muddy water tank 1, 14 electrode panel elements 4 are arranged by a support mechanism described below. The electrode panel elements 4 are vertically inserted in the tank, are orthogonal to the longitudinal direction of the muddy water tank 1, and are arranged substantially in parallel at regular intervals.

【0013】電極パネルエレメント4はほぼ正方形に裁
断されたエキスパンドメタルからなり、パネルフレーム
5に取り付けられている。個々のパネルフレーム5の上
部には両側に長く突出した個別桟6が取り付けられ、そ
の個別桟6がエレメント全体を支持する支持ベース桟7
に取り付けられている。支持ベース桟7は泥水槽1の上
端縁部に載置されるようにセットされる。この支持ベー
ス桟7に個別桟6が掛け渡されるようにセットされ、個
別桟6の下方にパネルフレーム5が吊り下げられた状態
となり、パネルフレーム5の枠内に電極パネルエレメン
ト4が取り付けられている。
The electrode panel element 4 is made of expanded metal cut into a substantially square shape, and is attached to the panel frame 5. On the upper part of each panel frame 5, an individual bar 6 projecting long on both sides is attached, and the individual bar 6 supports the entire base element 7
Is attached to. The support base rail 7 is set so as to be placed on the upper edge of the muddy water tank 1. The support rails 7 are set so that the individual rails 6 are hung, the panel frame 5 is suspended below the individual rails 6, and the electrode panel element 4 is mounted in the frame of the panel frame 5. There is.

【0014】泥水槽1内に配列された15枚の電極パネ
ルエレメント4が、以下に説明する配線機構による接続
を除いて、個々に電気的に絶縁されるように、支持ベー
ス桟7を絶縁材で構成したり、あるいは支持ベース桟7
と個別桟6の接触部分に絶縁材を介在させるなどの手段
を講じる。このように、各電極パネルエレメント4を個
々に絶縁した状態で、各エレメント4と直流電源8とを
極性切換器10を介して配電ケーブル9で接続する。
The support base rails 7 are made of an insulating material so that the fifteen electrode panel elements 4 arranged in the muddy water tank 1 are individually electrically insulated except for the connection by the wiring mechanism described below. Or support base bar 7
Means such as interposing an insulating material at the contact portion of the individual crosspiece 6 are taken. In this manner, each electrode panel element 4 is individually insulated, and each element 4 and the DC power source 8 are connected by the power distribution cable 9 via the polarity switcher 10.

【0015】また、泥水槽1の底部は谷形になってお
り、その底部に沿ってスクリューコンベア11が配設さ
れている。このスクリューコンベア11はモータ15で
駆動され、泥水槽1の底に沈澱した固形物を図2の左か
ら右へと搬送する。スクリューコンベア11の右側端部
は泥水槽1の側方にパイプ状に突出しており、その部分
に連結して縦形スクリューコンベア12がほぼ垂直に配
設されている。この縦形スクリューコンベア12はモー
タ13で駆動され、前記スクリューコンベア11で搬送
されてきた沈澱物を上方へ搬送する。縦形コンベア12
の搬出口12aは泥水槽1の水面より高く設定されてお
り、縦形コンベア12で搬送されてきた沈澱物は泥水と
分離されて搬出口12aからその直下のベルトコンベア
14上に落下し、所定の堆積場所へと搬送される。
The bottom of the muddy water tank 1 has a valley shape, and the screw conveyor 11 is arranged along the bottom. The screw conveyor 11 is driven by a motor 15 and conveys the solid matter deposited on the bottom of the muddy water tank 1 from left to right in FIG. The right end portion of the screw conveyor 11 projects laterally of the muddy water tank 1 in a pipe shape, and a vertical screw conveyor 12 is connected to the portion and is arranged substantially vertically. The vertical screw conveyor 12 is driven by a motor 13 and conveys the precipitate conveyed by the screw conveyor 11 upward. Vertical conveyor 12
Is set higher than the water surface of the muddy water tank 1, and the precipitate conveyed by the vertical conveyor 12 is separated from the muddy water and drops from the carry-out outlet 12a onto the belt conveyor 14 immediately below the muddy water. Transported to the deposition site.

【0016】以上のように構成された分離装置の動作と
使用方法について説明する。この分離装置は地盤掘削用
泥水の処理プラントにおける二次処理手段となる。前述
したように一次処理により礫、砂、および粘土・シルト
塊などの粗大分を分離除去した泥水を入口2から泥水槽
1に供給する。この泥水槽1における二次処理は、バッ
チ式でも良いし、連続フロー式でも良い。バッチ式の場
合、一次処理後の泥水を槽内に満たした状態で、直流電
源8から電極パネルエレメント4群に通電する。すると
泥水槽1内で正電極および負電極となって対向している
各電極パネルエレメント4の間隔部分で電気泳動現象が
起き、泥水にコロイド状に含まれている粘土・シルトな
どの超微粒子が正電極エレメント4側に移動して吸着
し、エキスパンドメタルからなる電極パネルエレメント
4の表面に超微粒子の凝集塊が成長する。したがって槽
1内の泥水は徐々に澄んでくる。
The operation and usage of the separating device configured as described above will be described. This separation device serves as a secondary treatment means in a treatment plant for ground mud. As described above, muddy water from which gravel, sand, and coarse particles such as clay / silt lumps have been separated and removed by the primary treatment is supplied from the inlet 2 to the muddy water tank 1. The secondary treatment in the muddy water tank 1 may be a batch type or a continuous flow type. In the case of the batch system, the DC power supply 8 energizes the electrode panel element group 4 in a state where the tank is filled with the muddy water after the primary treatment. Then, an electrophoretic phenomenon occurs in the space between the electrode panel elements 4 facing each other in the muddy water tank 1 as a positive electrode and a negative electrode, and ultrafine particles such as clay and silt contained in colloidal form in the muddy water. It moves toward the positive electrode element 4 side and is adsorbed, and an aggregate of ultrafine particles grows on the surface of the electrode panel element 4 made of expanded metal. Therefore, the muddy water in the tank 1 gradually becomes clear.

【0017】ある印加極性で通電を続けると、正電極エ
レメントに付着して成長する凝集塊が相当大きく厚くな
り、それ以上の凝集を効率よく行えなくなる。そのよう
になる前の適切な時点で、極性切換器10で電極パネル
エレメント4群への直流電圧の印加極性を反転させ、超
微粒子が凝集しているエレメントを負電極に切り換え、
これに対向しているエレメントを正電極に切り換える。
すると、エレメントに付着して大きくなった凝集塊が塊
のままでエレメントから脱落し、泥水槽1の底に沈澱す
る。また、このときから正電極になったエレメントの表
面に新たに超微粒子が凝集しはじめる。つまり、電極パ
ネルエレメント4群のひとつおきの半分づつが交互に正
電極になり、一方の群に超微粒子が凝集している過程
で、他方の群では直前までに付着成長した凝集塊が脱落
することになる。この動作を適宜時間おきに交互に繰り
返す。
When current is continuously applied with a certain applied polarity, the agglomerates attached to and grown on the positive electrode element become considerably large and thick, and further agglomeration cannot be performed efficiently. At an appropriate point before such a case, the polarity switching device 10 reverses the polarity of the DC voltage applied to the electrode panel element 4 group, and the element in which the ultrafine particles are aggregated is switched to the negative electrode.
The element facing this is switched to the positive electrode.
Then, the agglomerated lumps adhering to the element and growing, fall out of the element as lumps and settle on the bottom of the muddy water tank 1. Also, from this time, ultrafine particles newly start to aggregate on the surface of the element that has become the positive electrode. That is, every other half of the electrode panel element 4 group alternately becomes positive electrodes, and in the process in which the ultrafine particles are aggregated in one group, the aggregates that have adhered and grown up to immediately before in the other group fall off. It will be. This operation is alternately repeated at appropriate intervals.

【0018】また前記の処理によって充分に澄んだ処理
後の水を適宜な時点で出口3から排出する。なお、連続
フロー式で処理を行う場合は、入口2から出口3へきわ
めてゆっくりと泥水を供給し、処理前の泥水と処理後の
水とが混じり合わずに徐々に流れるようにする。
The treated water, which is sufficiently clear by the above treatment, is discharged from the outlet 3 at an appropriate time. When the treatment is carried out by the continuous flow method, the muddy water is supplied from the inlet 2 to the outlet 3 very slowly so that the muddy water before the treatment and the water after the treatment gradually flow without being mixed with each other.

【0019】泥水槽1の底部にある程度の量の固形物
(前記の凝集塊)が溜まったならば、スクリューコンベ
ア11、縦形スクリューコンベア12、ベルトコンベア
14を駆動し、その沈澱物を槽外へ排出する。ここで、
スクリューコンベア12を負に印加すれば超微粒子の凝
集塊が付着することが抑えられ、また、付着した凝集塊
を除去しやすい。
When a certain amount of solid matter (the above-mentioned aggregate) is accumulated at the bottom of the muddy water tank 1, the screw conveyor 11, the vertical screw conveyor 12, and the belt conveyor 14 are driven to move the precipitate to the outside of the tank. Discharge. here,
If the screw conveyor 12 is applied negatively, it is possible to suppress the attachment of the agglomerates of ultrafine particles, and it is easy to remove the attached agglomerates.

【0020】電極パネルエレメント4は実施例で説明し
たような格子状あるいは網目状の構造体が良い。多数の
電極パネルエレメントを泥水槽内に配列しても、エレメ
ントが格子状あるいは網目状の構造であれば、槽内の水
の流動性はあまり妨げられないし、電極表面積も大きく
なり、かつ電極表面に凝集する超微粒子の塊が安定に付
着することになる。電極パネルエレメントに適した材料
としては、前記のエキスパンドメタルの他、グレーティ
ングやパンチングメタルなどがある。
The electrode panel element 4 preferably has a lattice-like or mesh-like structure as described in the embodiment. Even if a large number of electrode panel elements are arranged in a muddy water tank, if the elements have a grid or mesh structure, the fluidity of water in the tank is not significantly hindered, the electrode surface area is large, and the electrode surface Agglomerates of ultra-fine particles that aggregate in a stable manner adhere to each other. Suitable materials for the electrode panel element include gratings and punching metals in addition to the expanded metal described above.

【0021】なお、以上説明した分離装置の実施例では
泥水槽に沈澱物排出用のスクリューコンベアを一体的に
設けているが、この発明の分離方法はこのような装置形
態でなくても効果的に実施することができる。印加電圧
を切り換えることで付着していた凝集塊はすぐにエレメ
ントから脱落するので、その後は電極パネルエレメント
4群を一体的に別の泥水槽に移し、その水槽内の泥水を
処理することとし、それまでの水槽の沈澱物の排出処理
は別途に行ってもよい。
In the embodiment of the separating apparatus described above, the muddy water tank is integrally provided with the screw conveyor for discharging the sediment, but the separating method of the present invention is effective even if it is not such an apparatus form. Can be carried out. The agglomerates attached by switching the applied voltage immediately fall off from the element, so after that, the electrode panel element 4 group is integrally moved to another muddy water tank, and the muddy water in the water tank is treated. The discharge treatment of the precipitate in the water tank until then may be performed separately.

【0022】[0022]

【発明の効果】以上詳細に説明したように、この発明に
よれば、電気泳動現象により泥水中の超微粒子を電極に
凝集させて能率よく分離することができるとともに、電
極への印加電圧の極性を切り換えるという非常に簡単な
手段で、電極に付着した超微粒子の凝集塊をすばやく取
り除くことができる。すなわち、泥水中の超微粒子を電
極に凝集させることと、その凝集塊を電極から塊のまま
で脱落させることとを一貫してきわめて能率よく行うこ
とができ、地盤掘削現場で次々に発生する大量の泥水を
処理する泥水処理プラントを実現することができる。
As described in detail above, according to the present invention, it is possible to efficiently separate the ultrafine particles in the mud water on the electrode by the electrophoretic phenomenon, and to polarize the voltage applied to the electrode. It is possible to quickly remove the agglomerates of ultrafine particles adhering to the electrodes by a very simple means of switching. That is, it is possible to consistently and extremely efficiently aggregate the ultrafine particles in the muddy water to the electrode and drop the aggregated mass from the electrode as it is. It is possible to realize a muddy water treatment plant that treats the muddy water.

【図面の簡単な説明】[Brief description of drawings]

【図1】この発明の一実施例による分離装置の平面図で
ある。
FIG. 1 is a plan view of a separation device according to an embodiment of the present invention.

【図2】同上実施例装置の正面図である。FIG. 2 is a front view of the above-mentioned embodiment apparatus.

【図3】同上実施例装置の側面図である。FIG. 3 is a side view of the apparatus according to the above embodiment.

【図4】同上実施例装置における電極パネルエレメント
部分の詳細図である。
FIG. 4 is a detailed view of an electrode panel element portion in the device of the above embodiment.

【符号の説明】[Explanation of symbols]

1 泥水槽 2 入口 3 出口 4 電極パネルエレメント 5 パネルフレーム 6 個別桟 7 支持ベース桟 8 直流電源 9 配電ケーブル 10 極性切換器 11 スクリューコンベア 12 縦形スクリューコンベア 13 モータ 14 ベルトコンベア 15 モータ 1 Muddy Water Tank 2 Inlet 3 Outlet 4 Electrode Panel Element 5 Panel Frame 6 Individual Rail 7 Support Base Rail 8 DC Power Supply 9 Distribution Cable 10 Polarity Switch 11 Screw Conveyor 12 Vertical Screw Conveyor 13 Motor 14 Belt Conveyor 15 Motor

───────────────────────────────────────────────────── フロントページの続き (72)発明者 吉崎 正明 東京都千代田区神田司町2丁目3番地 株 式会社大林組東京本社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Masaaki Yoshizaki 2-3 Kandaji-cho, Chiyoda-ku, Tokyo Obayashi Corporation Tokyo Head Office

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 泥水が入った水槽内に複数の電極パネル
エレメントを配設し、泥水中で対向する前記電極パネル
エレメント間に直流電圧を印加し、泥水中の超微粒子を
電気泳動現象により正電極となっている前記エレメント
の表面に凝集させ、前記エレメントに付着した凝集塊が
大きく成長した後に前記直流電圧の印加極性を反転し、
前記凝集塊が付着した前記エレメントを正電極から負電
極に変えることで、前記凝集塊を前記エレメント表面か
ら脱落させて前記水槽底に沈澱させることを特徴とする
地盤掘削用泥水処理プラントにおける超微粒子の分離方
法。
1. A plurality of electrode panel elements are arranged in a water tank containing mud water, a DC voltage is applied between the electrode panel elements facing each other in the mud water, and ultrafine particles in the mud water are corrected by an electrophoretic phenomenon. Aggregate on the surface of the element that is an electrode, reverse the applied polarity of the DC voltage after the agglomerate attached to the element grows large,
By changing the element to which the agglomerate is attached from a positive electrode to a negative electrode, the agglomerate is dropped from the surface of the element and settles on the bottom of the water tank, ultrafine particles in a mud treatment plant for ground excavation. Separation method.
【請求項2】 処理対象泥水が供給される水槽と、この
水槽内に配設された複数の電極パネルエレメントと、隣
り合って対向する前記電極パネルエレメント間に直流電
圧を印加するための直流電源と、この直流電源から前記
電極パネルエレメント間に印加する直流電圧の極性を切
り換えるための切り換え手段と、前記水槽の底部の沈澱
物を当該水槽外に排出する手段とを備えたことを特徴と
する地盤掘削用泥水処理プラントにおける超微粒子の分
離装置。
2. A DC tank for supplying muddy water to be treated, a plurality of electrode panel elements arranged in the tank, and a DC power source for applying a DC voltage between the adjacent electrode panel elements. And switching means for switching the polarity of the DC voltage applied from the DC power supply between the electrode panel elements, and means for discharging the precipitate at the bottom of the water tank to the outside of the water tank. Separation device for ultra-fine particles in a mud treatment plant for ground excavation.
JP30567692A 1992-11-16 1992-11-16 Method and apparatus for separating ultrafine particles in a muddy water treatment plant for ground excavation Expired - Fee Related JP2943539B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30567692A JP2943539B2 (en) 1992-11-16 1992-11-16 Method and apparatus for separating ultrafine particles in a muddy water treatment plant for ground excavation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30567692A JP2943539B2 (en) 1992-11-16 1992-11-16 Method and apparatus for separating ultrafine particles in a muddy water treatment plant for ground excavation

Publications (2)

Publication Number Publication Date
JPH06154762A true JPH06154762A (en) 1994-06-03
JP2943539B2 JP2943539B2 (en) 1999-08-30

Family

ID=17948016

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2943539B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100439431B1 (en) * 2001-07-31 2004-07-15 한국정수공업 주식회사 Method and Device for manufacturing the electrode cell of electrophoresis
US20120292186A1 (en) * 2011-05-17 2012-11-22 James Sidney Adamson Clarification of Tailing Ponds Using Electrophoresis
US9428408B2 (en) 2013-10-07 2016-08-30 Dpra Canada Incorporated Method and apparatus for treating tailings using an AC voltage with a DC offset
US9896356B2 (en) 2011-04-07 2018-02-20 Electro-Kinetic Solutions Inc. Electrokinetic process for consolidation of oil sands tailings

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100439431B1 (en) * 2001-07-31 2004-07-15 한국정수공업 주식회사 Method and Device for manufacturing the electrode cell of electrophoresis
US9896356B2 (en) 2011-04-07 2018-02-20 Electro-Kinetic Solutions Inc. Electrokinetic process for consolidation of oil sands tailings
US20120292186A1 (en) * 2011-05-17 2012-11-22 James Sidney Adamson Clarification of Tailing Ponds Using Electrophoresis
US9428408B2 (en) 2013-10-07 2016-08-30 Dpra Canada Incorporated Method and apparatus for treating tailings using an AC voltage with a DC offset

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Publication number Publication date
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